The feasibility of bench scale sequencing batch reactors (SBRs) in treating
a bottling plant effluent is demonstrated at various influent chemical oxy
gen demands (CODs) ranging from 300 to over 4,000 mg/L. The SBRs removed ov
er 75% of the biodegradable fraction of the influent COD at a fixed react t
ime of 5.5 h. An easy to use process model is presented to predict the temp
oral variations of substrate, biomass, and dissolved oxygen concentrations
during the fill and react periods in SBRs. The model satisfactorily predict
ed effluent COD and final biomass concentrations, as well as temporal varia
tions of COD, biomass, and dissolved oxygen throughout the fill and react c
ycles.